EP1411105A2 - Fuel additive compositions and fuel compositions containing detergents and fluidizers - Google Patents

Fuel additive compositions and fuel compositions containing detergents and fluidizers Download PDF

Info

Publication number
EP1411105A2
EP1411105A2 EP20030027271 EP03027271A EP1411105A2 EP 1411105 A2 EP1411105 A2 EP 1411105A2 EP 20030027271 EP20030027271 EP 20030027271 EP 03027271 A EP03027271 A EP 03027271A EP 1411105 A2 EP1411105 A2 EP 1411105A2
Authority
EP
European Patent Office
Prior art keywords
fuel
hydrocarbyl
fuel additive
polyether
additive composition
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP20030027271
Other languages
German (de)
French (fr)
Other versions
EP1411105A3 (en
EP1411105B9 (en
EP1411105B1 (en
Inventor
Malcolm G.J. Macduff
Rodney J Mcatee
Mitchell M Jackson
David C. Arters
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Lubrizol Corp
Original Assignee
Lubrizol Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=24065392&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP1411105(A2) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Lubrizol Corp filed Critical Lubrizol Corp
Publication of EP1411105A2 publication Critical patent/EP1411105A2/en
Publication of EP1411105A3 publication Critical patent/EP1411105A3/en
Application granted granted Critical
Publication of EP1411105B1 publication Critical patent/EP1411105B1/en
Publication of EP1411105B9 publication Critical patent/EP1411105B9/en
Anticipated expiration legal-status Critical
Revoked legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/238Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/143Organic compounds mixtures of organic macromolecular compounds with organic non-macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/146Macromolecular compounds according to different macromolecular groups, mixtures thereof
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/04Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/06Use of additives to fuels or fires for particular purposes for facilitating soot removal
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/16Hydrocarbons
    • C10L1/1616Hydrocarbons fractions, e.g. lubricants, solvents, naphta, bitumen, tars, terpentine
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/198Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
    • C10L1/1985Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid polyethers, e.g. di- polygylcols and derivatives; ethers - esters
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/238Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/2383Polyamines or polyimines, or derivatives thereof (poly)amines and imines; derivatives thereof (substituted by a macromolecular group containing 30C)

Definitions

  • the present invention involves fuel additive compositions and fuel compositions containing these fuel additive compositions.
  • the compositions are effective in reducing intake valve deposits of internal-combustion engines.
  • Deposits in the fuel delivery system and combustion chamber of an internal combustion engine can adversely effect combustion performance in terms of power output and emissions. Consequently, development of more effective fuel additives to prevent and/or reduce deposits is highly desirable.
  • the present invention provides deposit control fuel additive compositions exhibiting unexpectedly superior results that combine a Mannich detergent with a polyetheramine fluidizer or a polyether fluidizer or a mixture of polyetheramine and polyether fluidizers and, optionally, a succinimide detergent.
  • the fuel additive composition of the present invention comprises
  • Another aspect of the present invention is a fuel composition
  • a fuel composition comprising a mixture of a hydrocarbon fuel and the above-described fuel additive composition where the concentration of the Mannich detergent and the polyetheramine fluidizer combined on an actives basis is from 10 to 2000 ppm by weight.
  • a further embodiment of the present invention is the above-described fuel additive composition where the weight ratio on an actives basis of the Mannich detergent to the polyetheramine fluidizer is about 1:0.1-3.
  • Another embodiment of the present invention is a fuel composition
  • a fuel composition comprising a mixture of a hydrocarbon fuel, hydrocarbon solvent and the above-described fuel additive composition where the weight ratio on an actives basis of the Mannich detergent to the polyetheramine fluidizer is about 1:0.1-3 and the concentration of the detergent and the fluidizer combined is from 10 to 2000 ppm by weight on an actives basis.
  • the fuel additive composition comprises
  • the fuel additive composition comprises
  • An additional embodiment of the present invention is a fuel additive composition
  • a fuel additive composition comprising
  • the fuel additive composition comprises
  • a resulting embodiment of the present invention is a fuel composition
  • a fuel composition comprising a mixture of a hydrocarbon fuel, hydrocarbon solvent and the above-described fuel additive composition of Mannich detergent, polyether fluidizer and optionally succinimide detergent having a weight ratio on an actives basis of detergent(s) to fluidizer of about 1:0.5-2 where the concentration of detergent(s) and fluidizer combined is from 10 to 2000 ppm by weight on an actives basis.
  • the fuel additive composition comprises
  • a further resulting embodiment of the present invention is a fuel composition
  • a fuel composition comprising a mixture of a hydrocarbon fuel and the above-described fuel additive composition of Mannich detergent prepared from polyisobutylene-derived alkylphenol and formaldehyde and ethylenediamine, polyether fluidizer and optionally succinimide detergent where the concentration of detergent(s) and fluidizer combined is from 10 to 2000 ppm by weight on an actives basis.
  • the fuel additive composition of Mannich detergent prepared from phenol alkylated with 500 to 3000 number average molecular weight polyisobutylene having at least 70% vinylidene isomer content and formaldehyde and ethylenediamine, polyether fluidizer and optional succinimide detergent has a weight ratio of detergent(s) to fluidizer of about 1:0.5-2 on an actives basis.
  • the fuel additive compositions of the present invention comprise as a first component a Mannich reaction product of a hydrocarbyl-substituted phenol, an aldehyde, and an amine where the hydrocarbyl substituent has a number average molecular weight from 500 to 3000.
  • the hydrocarbyl substituent is a univalent radical of one or more carbon atoms that is predominately hydrocarbon in nature, but can have nonhydrocarbon substituent groups and can contain heteroatoms. This description of a hydrocarbyl substituent or group applies throughout the application.
  • the hydrocarbyl substituents are generally derived from polyolefins having a number average molecular weight of from 500 to 3000, preferably 700 to 2300, and most preferably 750 to 1500.
  • the polyolefins are generally derived from polymerization of olefin monomers including ethylene, propylene and various butene isomers including isobutylene.
  • the hydrocarbyl-substituted phenols can be obtained by alkylating phenol with a polyolefin using an alkylation catalyst such as boron trifluoride.
  • Polyisobutylenes can be used to alkylate phenol, and more preferably highly reactive polyisobutylene is used in the alkylation in which at least 70% of the terminal olefinic double bonds in the polyisobutylene are of the vinylidene type.
  • Commercial examples of highly reactive or high vinylidene polyisobutylenes include Ultravis®, formerly marketed by BP Chemical, and Glissopal® marketed by BASF.
  • the aldehyde is preferably a C 1 -C 6 aldehyde, the most preferred is formaldehyde that may be used in one of its reagent forms such as paraformaldehyde and formalin.
  • the amine can be a monoamine or a polyamine and includes organic compounds containing at least one HN ⁇ group suitable for use in the Mannich reaction.
  • Polyamines include alkylene polyamines such as ethylenediamine, diethylenetriamine and dimethylaminopropylamine.
  • the fuel additive compositions of the present invention comprise as a second component a fluidizer, for valve stick performance requirements, that can be a polyetheramine or a polyether or a mixture thereof.
  • the polyetheramines of the present invention are represented by the formula R[OCH 2 CH(R 1 )] n A where R is a hydrocarbyl group, R 1 is selected from the group consisting of hydrogen, hydrocarbyl groups of 1 to 16 carbon atoms, and mixtures thereof, n is a number from 2 to about 50, and A is selected from the group consisting of -OCH 2 CH 2 CH 2 NR 2 R 2 and -NR 3 R 3 where each R 2 is independently hydrogen or hydrocarbyl, and each R 3 is independently hydrogen, hydrocarbyl or -[R 4 N(R 5 )] p R 6 where R 4 is C 2 -C 10 alkylene, R 5 and R 6 are independently hydrogen or hydrocarbyl, and p is a number from 1-7.
  • polyetheramines can be prepared by initially condensing an alcohol or alkylphenol with an alkylene oxide, mixture of alkylene oxides or with several alkylene oxides in sequential fashion in a 1:2-50 mole ratio of hydric compound to alkylene oxide to form a polyether intermediate.
  • U.S. Patent 5,094,667 provides reaction conditions for preparing a polyether intermediate, the disclosure of which is incorporated herein by reference.
  • the alcohols can be linear or branched from 1 to 30 carbon atoms, more preferably from 6 to 20 carbon atoms, most preferably from 10 to 16 carbon atoms.
  • the alkyl group of the alkylphenols can be 1 to 30 carbon atoms, more preferably 10 to 20 carbon atoms.
  • the alkylene oxides are preferably ethylene oxide, propylene oxide or butylene oxide.
  • the number of alkylene oxide units in the polyether intermediate is preferably 10-35, more preferably 18-27.
  • the polyether intermediate can be converted to a polyetheramine by amination with ammonia, an amine or a polyamine to form a polyetheramine of the type where A is -NR 3 R 3 .
  • Published Patent Application EP310875 provides reaction conditions for the amination reaction, the disclosure of which is incorporated herein by reference.
  • the polyether intermediate can also be converted to a polyetheramine of the type where A is -OCH 2 CH 2 CH 2 NR 2 R 2 by reaction with acrylonitrile followed by hydrogenation.
  • U.S. Patent 5,094,667 provides reaction conditions for the cyanoethylation and subsequent hydrogenation, the disclosure of which is incorporated herein by reference.
  • Polyetheramines where A is -OCH 2 CH 2 CH 2 NH 2 are preferred.
  • Commercial examples of preferred polyetheramines are the Techron® range from Chevron and the Jeffamine® range from Huntsman.
  • the polyethers of the present invention are represented by the formula R 7 O[CH 2 CH(R 8 )O] q H where R 7 is a hydrocarbyl group, R 8 is selected from the group consisting of hydrogen, hydrocarbyl groups of 1 to 16 carbon atoms, and mixtures thereof, and q is a number from 2 to about 50.
  • Reaction conditions for preparation as well as preferred embodiments of the polyethers of the present invention were presented above in the polyetheramine description for the polyether intermediate.
  • a commercial example of preferred polyethers is the Lyondell ND® series. Suitable samples are also available from Dow Chemicals, Huntsman, and ICI.
  • the fuel compositions of the present invention comprise a mixture of the fuel additive composition as described throughout this description and a hydrocarbon fuel.
  • the hydrocarbon fuel is normally a liquid fuel, usually a hydrocarbonaceous petroleum distillate fuel such as motor gasoline as defined by ASTM Specification D439 or diesel fuel or fuel oil as defined by ASTM Specification D396.
  • Normally liquid fuel compositions comprising non-hydrocarbonaceous materials such as alcohols, ethers, organo-nitro compounds and the like (e.g., methanol, ethanol, diethyl ether, methyl ethyl ether, nitromethane) are also within the scope of this invention as are liquid fuels derived from vegetable or mineral sources such as corn, alfalfa, shale and coal.
  • gasoline that is, a mixture of hydrocarbons having an ASTM distillation range from about 60°C. at the 10% distillation point to about 205°C. at the 90% distillation point.
  • the fuel additive compositions of the present invention can also contain a hydrocarbon solvent to provide for their compatibility or homogeneity and to facilitate their handling and transfer.
  • the hydrocarbon solvent concentration in the fuel additive composition can be 10-80% by weight, preferably 20-70% by weight, and especially preferred being 30-60% by weight.
  • the hydrocarbon solvent can be an aliphatic fraction, aromatic fraction, or mixture of aliphatic and aromatic fractions where the flash point is generally about 40°C. or higher.
  • the hydrocarbon solvent is preferably an aromatic naphtha having a flash point above 62°C. or an aromatic naphtha having a flash point of 40°C. or a kerosene with a 16% aromatic content having a flash point above 62°C.
  • the fuel additive compositions of the present invention may contain as an optional component a succinimide prepared from a polyamine and a hydrocarbyl-substituted succinic acylating agent.
  • the hydrocarbyl substituent can have a number average molecular weight of about 500 to about 5000, preferably 750 to 1500.
  • the hydrocarbyl substituent can be derived from a polyolefin, preferably polyisobutylene.
  • the polyisobutylene preferably has at least 70% of its olefinic double bonds as the vinylidene isomer type.
  • the polyamine is preferably an alkylene polyamine to include alkylene polyamine bottoms.
  • the fuel additive composition comprises a Mannich reaction product detergent, a polyetheramine or polyether fluidizer or mixture thereof, and optionally a succinimide detergent in a weight ratio on an actives basis of detergent(s) to fluidizer(s) of about 1:0.1-3, more preferably 1:0.5-2, and most preferably 1:1-1.3.
  • the fuel composition comprises a mixture of a hydrocarbon fuel and a fuel additive composition comprising a Mannich reaction product detergent, a polyetheramine or polyether fluidizer or mixture thereof, and optionally a succinimide detergent where the concentration of the detergent(s) and fluidizer(s) combined on an actives basis is from 10 to 2000 ppm by weight, more preferably from 100 to 1000 ppm by weight, and most preferably from 150 to 400 ppm by weight.
  • the fuel additive compositions and fuel compositions of the present invention can contain other additives that are well known to those of skill in the art. These can include antiknock agents such as tetra-alkyl lead compounds and MMT (methylcyclopentadienyl manganese tricarbonyl), lead scavengers such as halo-alkanes, dyes, antioxidants such as hindered phenols, rust inhibitors such as alkylated succinic acids and anhydrides and derivatives thereof, bacteriostatic agents, auxiliary dispersants and detergents, gum inhibitors, fluidizer oils, metal deactivators, demulsifiers, anti-valve seat recession additives such as alkali metal sulphosuccinate salts, and anti-icing agents.
  • the fuel compositions of this invention can be lead-containing or lead-free fuels. Preferred are lead-free fuels.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

The present invention is directed to fuel additive compositions of detergents combined with fluidizers and to hydrocarbon fuel compositions containing these fuel additive compositions. The fuel additive compositions of the present invention combine a Mannich detergent, formed from reaction of an alkylphenol with an aldehyde and an amine, with a fluidizer that can be a polyether and, optionally, with a succinimide detergent. Fuel compositions containing these fuel additive compositions are very effective in reducing intake valve deposits in gasoline fueled engines, especially when the weight ratio of detergent(s) to fluidizer(s) is about 1:1 on an actives basis.

Description

    Background of the Invention 1. Field of the Invention
  • The present invention involves fuel additive compositions and fuel compositions containing these fuel additive compositions. The compositions are effective in reducing intake valve deposits of internal-combustion engines.
  • 2. Description of the Related Art
  • Deposits in the fuel delivery system and combustion chamber of an internal combustion engine can adversely effect combustion performance in terms of power output and emissions. Consequently, development of more effective fuel additives to prevent and/or reduce deposits is highly desirable.
  • Canadian Patent Publication 2,089,833, Graiff, August 21, 1993; U.S. Patent 5,697,988, Malfer et al., December 16, 1997; U.S. Patent 5,873,917, Daly, February 23, 1999; and U.S. Patent 5,876,468, Moreton, March 2, 1999, involve Mannich detergents, generally prepared by reaction of alkylphenols with aldehydes and amines, and polyether fluidizers for reduction of deposits in an engine combustion chamber and/or fuel delivery system.
  • U.S. Application Serial No. 09/337,997, McAtee, filed June 22, 1999, discloses hydrocarbon fuels containing a Mannich detergent composition including other compounds such as polyetheramines.
  • The present invention provides deposit control fuel additive compositions exhibiting unexpectedly superior results that combine a Mannich detergent with a polyetheramine fluidizer or a polyether fluidizer or a mixture of polyetheramine and polyether fluidizers and, optionally, a succinimide detergent.
  • Summary of the Invention
  • It is an object of this invention to reduce intake system deposits in hydrocarbon-fueled internal combustion engines.
  • It is a further object of this invention to reduce intake valve deposits in gasoline internal combustion engines.
  • Additional objects and advantages of the invention will be set forth in part in the description that follows and in part will be obvious from the description or may be learned by the practice of this invention. The objects and advantages of the invention may be realized and attained by means of the instrumentalities pointed out in the appended claims.
  • To achieve the foregoing objects in accordance with the invention, as described and claimed herein, the fuel additive composition of the present invention comprises
  • a) a Mannich detergent prepared from the reaction of a hydrocarbylphenol, an aldehyde and an amine where the hydrocarbyl substituent has a number average molecular weight of from 500 to 3000, and
  • b) a polyetheramine fluidizer of formula R[OCH2CH(R1)]nA where R is a hydrocarbyl group, R1 is selected from the group consisting of hydrogen, hydrocarbyl groups of 1 to 16 carbon atoms and mixtures thereof, n is a number 2 to about 50, and A is selected from the group consisting of -OCH2CH2CH2NR2R2 and -NR3R3 where each R2 is independently hydrogen or hydrocarbyl, and each R3 is independently hydrogen, hydrocarbyl or -[R4N(R5)]pR6 where R4 is C2―C10 alkylene, R5 and R6 are independently hydrogen or hydrocarbyl and p is a number from 1-7.
  • Another aspect of the present invention is a fuel composition comprising a mixture of a hydrocarbon fuel and the above-described fuel additive composition where the concentration of the Mannich detergent and the polyetheramine fluidizer combined on an actives basis is from 10 to 2000 ppm by weight.
  • A further embodiment of the present invention is the above-described fuel additive composition where the weight ratio on an actives basis of the Mannich detergent to the polyetheramine fluidizer is about 1:0.1-3.
  • Another embodiment of the present invention is a fuel composition comprising a mixture of a hydrocarbon fuel, hydrocarbon solvent and the above-described fuel additive composition where the weight ratio on an actives basis of the Mannich detergent to the polyetheramine fluidizer is about 1:0.1-3 and the concentration of the detergent and the fluidizer combined is from 10 to 2000 ppm by weight on an actives basis.
  • In a still further embodiment of the present invention, the fuel additive composition comprises
  • a) a Mannich detergent from the reaction of a hydrocarbyl-substituted phenol, an aldehyde and an amine where the hydrocarbyl substituent is derived from a polyisobutylene having a number average molecular weight of from 500 to 3000 and a vinylidene isomer content of at least 70%, and
  • b) a polyetheramine fluidizer of the formula R[OCH2CH(R1)]nOCH2CH2CH2NH2 where R is C1-C30 alkyl group or C1-C30 alkyl-substituted phenyl group, R1 is hydrogen, methyl or ethyl, and n is a number from about 10 to about 35 where the weight ratio of the detergent to the fluidizer on an actives basis is about 1:0.5-2.
  • In yet another embodiment of the present invention, the fuel additive composition comprises
  • (a) a Mannich reaction product of a hydrocarbyl-substituted phenol where the hydrocarbyl substituent has a number average molecular weight of from 500 to 3000, an aldehyde, and an amine, and
  • (b) a polyetheramine represented by the formula R[OCH2CH(R1)]nA where R is a hydrocarbyl group, R1 is selected from the group consisting of hydrogen, hydrocarbyl groups of 1 to 16 carbon atoms, and mixtures thereof, n is a number from 2 to about 50, and A is selected from the group consisting of -OCH2CH2CH2NR2R2 and -NR3R3 where each R2 is independently hydrogen or hydrocarbyl, and each R3 is independently hydrogen, hydrocarbyl or -[R4N(R5)]pR6 where R4 is C2-C10 alkylene, R5 and R6 are independently hydrogen or hydrocarbyl, and p is a number from 1-7, and
  • (c) a polyether represented by the formula R7O[CH2CH(R8)O]qH where R7 is a hydrocarbyl group, R8 is selected from the group consisting of hydrogen, hydrocarbyl groups of 1 to 16 carbon atoms, and mixtures thereof, and q is a number from 2 to about 50.
  • An additional embodiment of the present invention is a fuel additive composition comprising
  • a) a Mannich detergent prepared from the reaction of a hydrocarbyl-substituted phenol, an aldehyde, and an amine where the hydrocarbyl substituent is derived from a polyisobutylene having a number average molecular weight molecular weight of from 500 to 3000 and a vinylidene isomer content of at least 70%, and
  • b) a polyether fluidizer of the formula R7O[CH2CH(R8)O]qH where R7 is a hydrocarbyl group, R8 is selected from the group consisting of hydrogen, hydrocarbyl groups of 1 to 16 carbon atoms, and mixtures thereof, and q is a number from 2 to about 50, and optionally
  • c) a succinimide detergent prepared from the reaction of a polyamine and a hydrocarbyl-substituted succinic acylating agent where the weight ratio of detergent(s) to fluidizer is about 1:0.5-2 on an actives basis.
  • In a further additional embodiment of the present invention, the fuel additive composition comprises
  • a) Mannich detergent prepared from the reaction of a hydrocarbyl-substituted phenol, an aldehyde, and an amine where the hydrocarbyl substituent is derived from a polyisobutylene having a number average molecular weight of from 500 to 3000 and a vinylidene isomer content of at least 70%, and
  • b) a polyether fluidizer of the formula R7O[CH2CH(R8)O]qH where R7 is a hydrocarbyl group, R8 is selected from the group consisting of hydrogen, hydrocarbyl groups of 1 to 16 carbon atoms, and mixtures thereof, and q is a number from 2 to about 50, and optionally
  • c) a succinimide detergent prepared from the reaction of a polyamine and a hydrocarbyl-substituted succinic acylating agent where the weight ratio of detergent(s) to fluidizer is about 1: 0.5-2 on an actives basis, and
  • d) a polyetheramine represented by the formula R[OCH2CH(R1)]nA wherein R is a hydrocarbyl group; R1 is selected from the group consisting of hydrogen, hydrocarbyl groups of 1 to 16 carbon atoms, and mixtures thereof; n is a number from 2 to about 50; and A is selected from the group consisting of -OCH2CH2CH2NR2R2 and -NR3R3 wherein each R2 is independently hydrogen or hydrocarbyl; and each R3 is independently hydrogen, hydrocarbyl or -[R4N(R5)]pR6 wherein R4 is C2-C10 alkylene; R5 and R6 are independently hydrogen or hydrocarbyl; and p is a number from 1-7.
  • A resulting embodiment of the present invention is a fuel composition comprising a mixture of a hydrocarbon fuel, hydrocarbon solvent and the above-described fuel additive composition of Mannich detergent, polyether fluidizer and optionally succinimide detergent having a weight ratio on an actives basis of detergent(s) to fluidizer of about 1:0.5-2 where the concentration of detergent(s) and fluidizer combined is from 10 to 2000 ppm by weight on an actives basis.
  • In a still additional embodiment of the present invention, the fuel additive composition comprises
  • a) a Mannich detergent prepared from a hydrocarbyl-substituted phenol, formaldehyde, and ethylenediamine where the hydrocarbyl substitutent is derived from a polyisobutylene having a number average molecular weight of from 500 to 3000 and a vinylidene isomer content of at least 70%, and
  • b) a polyether fluidizer of the formula R7O[CH2CH(R8)O]qH where R7 is a C1-C30 alkyl group or a C1-C30 alkyl-substituted phenyl group, R8 is hydrogen, methyl or ethyl, and q is a number from about 10 to about 35, and optionally
  • c) a succinimide detergent prepared from a polyamine and a hydrocarbyl-substituted succinic acylating agent.
  • A further resulting embodiment of the present invention is a fuel composition comprising a mixture of a hydrocarbon fuel and the above-described fuel additive composition of Mannich detergent prepared from polyisobutylene-derived alkylphenol and formaldehyde and ethylenediamine, polyether fluidizer and optionally succinimide detergent where the concentration of detergent(s) and fluidizer combined is from 10 to 2000 ppm by weight on an actives basis.
  • Finally in another embodiment of the present invention, the fuel additive composition of Mannich detergent, prepared from phenol alkylated with 500 to 3000 number average molecular weight polyisobutylene having at least 70% vinylidene isomer content and formaldehyde and ethylenediamine, polyether fluidizer and optional succinimide detergent has a weight ratio of detergent(s) to fluidizer of about 1:0.5-2 on an actives basis.
  • Detailed Description of the Invention
  • The fuel additive compositions of the present invention comprise as a first component a Mannich reaction product of a hydrocarbyl-substituted phenol, an aldehyde, and an amine where the hydrocarbyl substituent has a number average molecular weight from 500 to 3000.
  • The hydrocarbyl substituent is a univalent radical of one or more carbon atoms that is predominately hydrocarbon in nature, but can have nonhydrocarbon substituent groups and can contain heteroatoms. This description of a hydrocarbyl substituent or group applies throughout the application. The hydrocarbyl substituents are generally derived from polyolefins having a number average molecular weight of from 500 to 3000, preferably 700 to 2300, and most preferably 750 to 1500. The polyolefins are generally derived from polymerization of olefin monomers including ethylene, propylene and various butene isomers including isobutylene. The hydrocarbyl-substituted phenols can be obtained by alkylating phenol with a polyolefin using an alkylation catalyst such as boron trifluoride. Polyisobutylenes can be used to alkylate phenol, and more preferably highly reactive polyisobutylene is used in the alkylation in which at least 70% of the terminal olefinic double bonds in the polyisobutylene are of the vinylidene type. Commercial examples of highly reactive or high vinylidene polyisobutylenes include Ultravis®, formerly marketed by BP Chemical, and Glissopal® marketed by BASF.
  • The aldehyde is preferably a C1-C6 aldehyde, the most preferred is formaldehyde that may be used in one of its reagent forms such as paraformaldehyde and formalin.
  • The amine can be a monoamine or a polyamine and includes organic compounds containing at least one HN< group suitable for use in the Mannich reaction. Polyamines include alkylene polyamines such as ethylenediamine, diethylenetriamine and dimethylaminopropylamine.
  • The conditions required for Mannich reactions to form the Mannich reaction products of this invention are known in the art. For typical conditions for Mannich reactions see U.S. Patents 3,877,889, 5,697,988 and 5,876,468, the disclosures of which are incorporated herein by reference.
  • The fuel additive compositions of the present invention comprise as a second component a fluidizer, for valve stick performance requirements, that can be a polyetheramine or a polyether or a mixture thereof.
  • The polyetheramines of the present invention are represented by the formula R[OCH2CH(R1)]nA where R is a hydrocarbyl group, R1 is selected from the group consisting of hydrogen, hydrocarbyl groups of 1 to 16 carbon atoms, and mixtures thereof, n is a number from 2 to about 50, and A is selected from the group consisting of -OCH2CH2CH2NR2R2 and -NR3R3 where each R2 is independently hydrogen or hydrocarbyl, and each R3 is independently hydrogen, hydrocarbyl or -[R4N(R5)]pR6 where R4 is C2-C10 alkylene, R5 and R6 are independently hydrogen or hydrocarbyl, and p is a number from 1-7.
  • These polyetheramines can be prepared by initially condensing an alcohol or alkylphenol with an alkylene oxide, mixture of alkylene oxides or with several alkylene oxides in sequential fashion in a 1:2-50 mole ratio of hydric compound to alkylene oxide to form a polyether intermediate. U.S. Patent 5,094,667 provides reaction conditions for preparing a polyether intermediate, the disclosure of which is incorporated herein by reference.
  • The alcohols can be linear or branched from 1 to 30 carbon atoms, more preferably from 6 to 20 carbon atoms, most preferably from 10 to 16 carbon atoms. The alkyl group of the alkylphenols can be 1 to 30 carbon atoms, more preferably 10 to 20 carbon atoms.
  • The alkylene oxides are preferably ethylene oxide, propylene oxide or butylene oxide. The number of alkylene oxide units in the polyether intermediate is preferably 10-35, more preferably 18-27.
  • The polyether intermediate can be converted to a polyetheramine by amination with ammonia, an amine or a polyamine to form a polyetheramine of the type where A is -NR3R3. Published Patent Application EP310875 provides reaction conditions for the amination reaction, the disclosure of which is incorporated herein by reference. Alternately, the polyether intermediate can also be converted to a polyetheramine of the type where A is -OCH2CH2CH2NR2R2 by reaction with acrylonitrile followed by hydrogenation. U.S. Patent 5,094,667 provides reaction conditions for the cyanoethylation and subsequent hydrogenation, the disclosure of which is incorporated herein by reference.
  • Polyetheramines where A is -OCH2CH2CH2NH2 are preferred. Commercial examples of preferred polyetheramines are the Techron® range from Chevron and the Jeffamine® range from Huntsman.
  • The polyethers of the present invention are represented by the formula R7O[CH2CH(R8)O]qH where R7 is a hydrocarbyl group, R8 is selected from the group consisting of hydrogen, hydrocarbyl groups of 1 to 16 carbon atoms, and mixtures thereof, and q is a number from 2 to about 50. Reaction conditions for preparation as well as preferred embodiments of the polyethers of the present invention were presented above in the polyetheramine description for the polyether intermediate. A commercial example of preferred polyethers is the Lyondell ND® series. Suitable samples are also available from Dow Chemicals, Huntsman, and ICI.
  • The fuel compositions of the present invention comprise a mixture of the fuel additive composition as described throughout this description and a hydrocarbon fuel. The hydrocarbon fuel is normally a liquid fuel, usually a hydrocarbonaceous petroleum distillate fuel such as motor gasoline as defined by ASTM Specification D439 or diesel fuel or fuel oil as defined by ASTM Specification D396. Normally liquid fuel compositions comprising non-hydrocarbonaceous materials such as alcohols, ethers, organo-nitro compounds and the like (e.g., methanol, ethanol, diethyl ether, methyl ethyl ether, nitromethane) are also within the scope of this invention as are liquid fuels derived from vegetable or mineral sources such as corn, alfalfa, shale and coal. Normally liquid fuels that are mixtures of one or more hydrocarbonaceous fuels and one or more non-hydrocarbonaceous materials are also contemplated. Examples of such mixtures are combinations of gasoline and ethanol and of diesel fuel and ether. Particularly preferred is gasoline, that is, a mixture of hydrocarbons having an ASTM distillation range from about 60°C. at the 10% distillation point to about 205°C. at the 90% distillation point.
  • The fuel additive compositions of the present invention can also contain a hydrocarbon solvent to provide for their compatibility or homogeneity and to facilitate their handling and transfer. The hydrocarbon solvent concentration in the fuel additive composition can be 10-80% by weight, preferably 20-70% by weight, and especially preferred being 30-60% by weight. The hydrocarbon solvent can be an aliphatic fraction, aromatic fraction, or mixture of aliphatic and aromatic fractions where the flash point is generally about 40°C. or higher. The hydrocarbon solvent is preferably an aromatic naphtha having a flash point above 62°C. or an aromatic naphtha having a flash point of 40°C. or a kerosene with a 16% aromatic content having a flash point above 62°C.
  • The fuel additive compositions of the present invention may contain as an optional component a succinimide prepared from a polyamine and a hydrocarbyl-substituted succinic acylating agent. The hydrocarbyl substituent can have a number average molecular weight of about 500 to about 5000, preferably 750 to 1500. The hydrocarbyl substituent can be derived from a polyolefin, preferably polyisobutylene. The polyisobutylene preferably has at least 70% of its olefinic double bonds as the vinylidene isomer type. The polyamine is preferably an alkylene polyamine to include alkylene polyamine bottoms. U.S. Patent 5,719,108 provides a general discussion on preparing hydrocarbyl-substituted succinic acylating agents, the disclosure of which is incorporated herein by reference.
  • In a preferred embodiment of the present invention, the fuel additive composition comprises a Mannich reaction product detergent, a polyetheramine or polyether fluidizer or mixture thereof, and optionally a succinimide detergent in a weight ratio on an actives basis of detergent(s) to fluidizer(s) of about 1:0.1-3, more preferably 1:0.5-2, and most preferably 1:1-1.3.
  • In another preferred embodiment of the present invention, the fuel composition comprises a mixture of a hydrocarbon fuel and a fuel additive composition comprising a Mannich reaction product detergent, a polyetheramine or polyether fluidizer or mixture thereof, and optionally a succinimide detergent where the concentration of the detergent(s) and fluidizer(s) combined on an actives basis is from 10 to 2000 ppm by weight, more preferably from 100 to 1000 ppm by weight, and most preferably from 150 to 400 ppm by weight.
  • The fuel additive compositions and fuel compositions of the present invention can contain other additives that are well known to those of skill in the art. These can include antiknock agents such as tetra-alkyl lead compounds and MMT (methylcyclopentadienyl manganese tricarbonyl), lead scavengers such as halo-alkanes, dyes, antioxidants such as hindered phenols, rust inhibitors such as alkylated succinic acids and anhydrides and derivatives thereof, bacteriostatic agents, auxiliary dispersants and detergents, gum inhibitors, fluidizer oils, metal deactivators, demulsifiers, anti-valve seat recession additives such as alkali metal sulphosuccinate salts, and anti-icing agents. The fuel compositions of this invention can be lead-containing or lead-free fuels. Preferred are lead-free fuels.
  • The following examples are set forth only for illustrative purposes.
  • The test results set forth in Table 1 and Table 2 below demonstrate the superior effectiveness of the fuel additive compositions and the fuel compositions of the present invention in controlling intake valve deposits (IVD) in engine testing.
    M102E Test1
    Example Detergent2, ppm Fluidizer, ppm IVD3, mg
    1 (comparati ve) 61 1334 209
    2 97 975 5
    3 97 976 52
    4 97 977 12
    5 97 974 170
    Renault Clio Field Test
    Example Mannich Detergent, ppm Succinimide Detergent, ppm Polyether Fluidizer, ppm IVD, mg
    6 (comparative) 90 --- 198 93
    7 144 --- 144 40
    8 113 31 144 26
    9 113 31 144 6.5
    10 72 72 144 0.5

Claims (7)

  1. A fuel additive composition, comprising:
    (a) a Mannich reaction product of a hydrocarbyl-substituted phenol wherein the hydrocarbyl substituent is derived from a polyisobutylene having a number average molecular weight of from 500 to 3000 and a vinylidene isomer content of at least 70%; an aldehyde; and an amine; and
    (b) a polyether represented by the formula R7O[CH2CH(R8)O]qH wherein R7 is a hydrocarbyl group; R8 is selected from the group consisting of hydrogen, hydrocarbyl groups of 1 to 16 carbon atoms, and mixtures thereof; and q is a number from 2 to about 50; and optionally
    (c) a succinimide prepared from a polyamine and a hydrocarbyl-substituted succinic acylating agent wherein the weight ratio of the Mannich reaction product and the succinimide combined to the polyether is about 1:0.5-2.
  2. The fuel additive composition of claim 1, further comprising:
    (e) a hydrocarbon solvent.
  3. A fuel composition, comprising:
    a hydrocarbon fuel; and
    the fuel additive composition of claim 2 wherein the concentration of the Mannich reaction product, the polyether and the succinimide combined is from 10 to 2000 ppm by weight.
  4. The fuel additive composition, of claim 1 wherein the aldehyde and the amine of the Mannich reaction product is formaldehyde and ethylenediamine; and R7 of the polyether is a C1-C30 alkyl group or a C1-C30 alkyl-substituted phenyl group; R8 is hydrogen, methyl or ethyl; and q is a number from about 10 to about 35.
  5. A fuel composition, comprising:
    a hydrocarbon fuel; and
    the fuel additive composition of claim 4 wherein the concentration of the Mannich reaction product, the polyether and the succinimide combined is from 10 to 2000 ppm by weight.
  6. The fuel additive composition of claim 4, further comprising:
    (d) a hydrocarbon solvent.
  7. A fuel composition, comprising:
    a hydrocarbon fuel; and
    the fuel additive composition of claim 4 wherein the concentration of the Mannich reaction product, the polyether and the succinimide combined is from 10 to 2000 ppm by weight.
EP03027271A 2000-03-03 2001-02-26 Fuel additive compositions and fuel compositions containing detergents and fluidizers Revoked EP1411105B9 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US518762 2000-03-03
US09/518,762 US6458172B1 (en) 2000-03-03 2000-03-03 Fuel additive compositions and fuel compositions containing detergents and fluidizers
EP01914524A EP1268715B1 (en) 2000-03-03 2001-02-26 Fuel additive compositions and fuel compositions containing detergents and fluidizers

Related Parent Applications (2)

Application Number Title Priority Date Filing Date
EP01914524A Division EP1268715B1 (en) 2000-03-03 2001-02-26 Fuel additive compositions and fuel compositions containing detergents and fluidizers
EP01914524A Division-Into EP1268715B1 (en) 2000-03-03 2001-02-26 Fuel additive compositions and fuel compositions containing detergents and fluidizers

Publications (4)

Publication Number Publication Date
EP1411105A2 true EP1411105A2 (en) 2004-04-21
EP1411105A3 EP1411105A3 (en) 2004-04-28
EP1411105B1 EP1411105B1 (en) 2009-07-08
EP1411105B9 EP1411105B9 (en) 2009-10-14

Family

ID=24065392

Family Applications (2)

Application Number Title Priority Date Filing Date
EP01914524A Revoked EP1268715B1 (en) 2000-03-03 2001-02-26 Fuel additive compositions and fuel compositions containing detergents and fluidizers
EP03027271A Revoked EP1411105B9 (en) 2000-03-03 2001-02-26 Fuel additive compositions and fuel compositions containing detergents and fluidizers

Family Applications Before (1)

Application Number Title Priority Date Filing Date
EP01914524A Revoked EP1268715B1 (en) 2000-03-03 2001-02-26 Fuel additive compositions and fuel compositions containing detergents and fluidizers

Country Status (6)

Country Link
US (1) US6458172B1 (en)
EP (2) EP1268715B1 (en)
AU (2) AU3990201A (en)
CA (1) CA2402851A1 (en)
DE (2) DE60139215D1 (en)
WO (1) WO2001066673A2 (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1518918A1 (en) * 2003-09-25 2005-03-30 Afton Chemical Corporation Fuels compositions and methods for using same
EP1840192A1 (en) 2006-03-30 2007-10-03 Afton Chemical Corporation Treated port fuel injectors
WO2009040583A1 (en) * 2007-09-27 2009-04-02 Innospec Limited Fuel compositions
WO2009040584A1 (en) * 2007-09-27 2009-04-02 Innospec Limited Fuel compositions
GB2453248B (en) * 2007-09-27 2011-11-23 Innospec Ltd Fuel compositions
CN106103667A (en) * 2013-11-18 2016-11-09 雅富顿化学公司 Cleanser compositions for the mixing that inlet valve deposits controls
US10273425B2 (en) 2017-03-13 2019-04-30 Afton Chemical Corporation Polyol carrier fluids and fuel compositions including polyol carrier fluids
US11795412B1 (en) 2023-03-03 2023-10-24 Afton Chemical Corporation Lubricating composition for industrial gear fluids
US11873461B1 (en) 2022-09-22 2024-01-16 Afton Chemical Corporation Extreme pressure additives with improved copper corrosion
US11884890B1 (en) 2023-02-07 2024-01-30 Afton Chemical Corporation Gasoline additive composition for improved engine performance
US12024686B2 (en) 2022-09-30 2024-07-02 Afton Chemical Corporation Gasoline additive composition for improved engine performance

Families Citing this family (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19948114A1 (en) 1999-10-06 2001-04-12 Basf Ag Process for the preparation of Mannich adducts containing polyisobutene phenol
DE19948111A1 (en) * 1999-10-06 2001-04-12 Basf Ag Process for the preparation of Mannich adducts containing polyisobutene phenol
US20030029077A1 (en) * 2001-08-07 2003-02-13 The Lubrizol Corporation, A Corporation Of The State Of Ohio Fuel composition containing detergent combination and methods thereof
US20050172544A1 (en) * 2002-02-19 2005-08-11 Macduff Malcolm G.J. Method for operating internal combustion engine with a fuel composition
US20030177692A1 (en) * 2002-03-12 2003-09-25 The Lubrizol Corporation Method of operating a direct injection spark-ignited engine with a fuel composition
US7795192B2 (en) * 2002-04-19 2010-09-14 The Lubrizol Corporation Lubricant composition suitable for direct fuel injected, crankcase-scavenged two-stroke engines
WO2003095595A1 (en) 2002-05-09 2003-11-20 The Lubrizol Corporation Continuously variable transmission fluids comprising a combination of calcium- and magnesium-overbased detergents
US20050257724A1 (en) * 2004-05-24 2005-11-24 Guinther Gregory H Additive-induced control of NOx emissions in a coal burning utility furnace
EP1812534B1 (en) * 2004-10-19 2016-10-05 The Lubrizol Corporation Additive and fuel compositions containing detergent and fluidizer and method thereof
JP5276327B2 (en) * 2005-02-18 2013-08-28 ザ ルブリゾル コーポレイション Multifunctional dispersant
JP5083968B2 (en) * 2005-02-18 2012-11-28 ザ ルブリゾル コーポレイション Lubricating additive formulations containing multifunctional dispersants
US20060196111A1 (en) * 2005-03-04 2006-09-07 Colucci William J Fuel additive composition
US20060277819A1 (en) * 2005-06-13 2006-12-14 Puri Suresh K Synergistic deposit control additive composition for diesel fuel and process thereof
US20060277820A1 (en) * 2005-06-13 2006-12-14 Puri Suresh K Synergistic deposit control additive composition for gasoline fuel and process thereof
US8222180B2 (en) * 2005-08-01 2012-07-17 Indian Oil Corporation Limited Adsorbent composition for removal of refractory sulphur compounds from refinery streams and process thereof
US7597726B2 (en) * 2006-01-20 2009-10-06 Afton Chemical Corporation Mannich detergents for hydrocarbon fuels
US20070245621A1 (en) * 2006-04-20 2007-10-25 Malfer Dennis J Additives for minimizing injector fouling and valve deposits and their uses
US20090298729A1 (en) 2006-04-24 2009-12-03 The Lubrizol Corporation Star Polymer Lubricating Composition
EP2661482B1 (en) 2011-01-04 2016-12-28 The Lubrizol Corporation Continuously variable transmission fluid with extended anti-shudder durability
US8915976B1 (en) * 2013-12-02 2014-12-23 Christopher Haydn Lowery Fuel additive
US11788463B2 (en) 2014-10-08 2023-10-17 Ats Chemical, Llc Compositions for engine carbon removal and methods and apparatus for removing carbon
EP3390594B1 (en) 2015-12-18 2022-06-29 The Lubrizol Corporation Nitrogen-functionalized olefin polymers for engine lubricants
CN110168063A (en) * 2017-01-17 2019-08-23 路博润公司 Engine lubricant containing polyether compound
CN113150856A (en) * 2018-03-30 2021-07-23 锦州惠发天合化学有限公司 Soot dispersants

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0569228A1 (en) * 1992-05-06 1993-11-10 Ethyl Petroleum Additives, Inc. Compositions for control of induction system deposits
EP0831141A1 (en) * 1996-09-05 1998-03-25 BP Chemicals (Additives) Limited Detergents for hydrocarbon fuels
EP0870819A2 (en) * 1997-04-10 1998-10-14 Ethyl Corporation Additives for minimizing intake valve deposits, and their use
EP1277828A2 (en) * 1999-02-09 2003-01-22 Basf Aktiengesellschaft Fuel composition

Family Cites Families (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4231759A (en) * 1973-03-12 1980-11-04 Standard Oil Company (Indiana) Liquid hydrocarbon fuels containing high molecular weight Mannich bases
US3877889A (en) * 1973-11-07 1975-04-15 Lubrizol Corp Liquid hydrocarbon fuels containing Mannich bases or derivatives thereof
US4298708A (en) 1979-04-02 1981-11-03 Texaco Development Corp. Aminated alkoxylated aliphatic alcohol salts as polyisocyanurate catalysts
US4332595A (en) 1980-12-05 1982-06-01 Texaco Inc. Ether amine detergent and motor fuel composition containing same
US4464182A (en) 1981-03-31 1984-08-07 Exxon Research & Engineering Co. Glycol ester flow improver additive for distillate fuels
US4396517A (en) 1981-08-10 1983-08-02 Mobil Oil Corporation Phenolic-containing mannich bases and lubricants containing same
US4604103A (en) 1982-07-30 1986-08-05 Chevron Research Company Deposit control additives--polyether polyamine ethanes
US4526587A (en) 1983-05-31 1985-07-02 Chevron Research Company Deposit control additives-methylol polyether amino ethanes
US4600409A (en) 1983-07-29 1986-07-15 Chevron Research Company Quaternary deposit control additives
US4564372A (en) 1983-07-29 1986-01-14 Chevron Research Company Quaternary deposit control additives
US4778481A (en) 1983-08-08 1988-10-18 Chevron Research Company Diesel fuel and method for deposit control in compression ignition engines
US4568358A (en) 1983-08-08 1986-02-04 Chevron Research Company Diesel fuel and method for deposit control in compression ignition engines
US4609377A (en) 1985-10-07 1986-09-02 Texaco Inc. Aminated polyisopropoxylated polyethoxylated alkylphenol and ethanol/gasoline blend composition containing same
DE68913849T2 (en) 1988-08-05 1994-09-22 Kao Corp Use of an additive for fuel.
DE3826608A1 (en) 1988-08-05 1990-02-08 Basf Ag FUELS CONTAINING POLYETHERAMINE OR POLYETHERAMINE DERIVATIVES FOR OTTO ENGINES
US4944770A (en) 1988-09-02 1990-07-31 Texaco, Inc. Motor fuel additive and ori-inhibited motor fuel composition
US4975096A (en) 1988-09-09 1990-12-04 Chevron Research Company Long chain aliphatic hydrocarbyl amine additives having an oxyalkylene hydroxy connecting group
US4964879A (en) 1989-03-27 1990-10-23 Texaco Inc. Middle distillate fuel containing deposit inhibitor
JPH0662965B2 (en) 1990-02-02 1994-08-17 花王株式会社 Fuel oil additive and fuel oil additive composition
US5264006A (en) 1990-03-20 1993-11-23 Exxon Research And Engineering Co. Guerbet alkyl ether mono amines
US5094667A (en) * 1990-03-20 1992-03-10 Exxon Research And Engineering Company Guerbet alkyl ether mono amines
US5242469A (en) 1990-06-07 1993-09-07 Tonen Corporation Gasoline additive composition
DE4038913A1 (en) 1990-12-06 1992-06-11 Basf Ag New alkoxylated polyether-di:amine cpd. - obtd. by amination of polyglycol and reacting with alkylene oxide, used in fuel for Otto engine
US5503644A (en) 1991-09-23 1996-04-02 Shell Oil Company Gasoline composition for reducing intake valve deposits in port fuel injected engines
US5697988A (en) 1991-11-18 1997-12-16 Ethyl Corporation Fuel compositions
CA2089833A1 (en) 1992-02-20 1993-08-21 Leonard Baldine Graiff Gasoline composition
US5192335A (en) 1992-03-20 1993-03-09 Chevron Research And Technology Company Fuel additive compositions containing poly(oxyalkylene) amines and polyalkyl hydroxyaromatics
US5387266A (en) 1993-06-11 1995-02-07 Ethyl Corporation Mannich base derivatives, and the production and uses thereof
DE69421784T2 (en) * 1993-10-06 2000-05-18 Ethyl Corp., Richmond Fuel compositions, and additives therefor
DE4432038A1 (en) 1994-09-09 1996-03-14 Basf Ag Fuels containing polyetheramines for gasoline engines
US5514190A (en) 1994-12-08 1996-05-07 Ethyl Corporation Fuel compositions and additives therefor
US5512067A (en) 1995-05-22 1996-04-30 Ethyl Corporation Asymmetrical mannich base derivatives and the production and uses thereof
US5634951A (en) * 1996-06-07 1997-06-03 Ethyl Corporation Additives for minimizing intake valve deposits, and their use
US5873917A (en) * 1997-05-16 1999-02-23 The Lubrizol Corporation Fuel additive compositions containing polyether alcohol and hydrocarbylphenol
US6217624B1 (en) 1999-02-18 2001-04-17 Chevron Chemical Company Llc Fuel compositions containing hydrocarbyl-substituted polyoxyalkylene amines
DE19916512A1 (en) 1999-04-13 2000-10-19 Basf Ag Polyalkene alcohol polyether amines and their use in fuels and lubricants
US6179885B1 (en) * 1999-06-22 2001-01-30 The Lubrizol Corporation Aromatic Mannich compound-containing composition and process for making same
CA2334508A1 (en) 2000-03-01 2001-09-01 Majid R. Ahmadi Fuel additive compositions containing mannich condensation products and hydrocarbyl-substituted polyoxyalkylene amines

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0569228A1 (en) * 1992-05-06 1993-11-10 Ethyl Petroleum Additives, Inc. Compositions for control of induction system deposits
EP0831141A1 (en) * 1996-09-05 1998-03-25 BP Chemicals (Additives) Limited Detergents for hydrocarbon fuels
EP0870819A2 (en) * 1997-04-10 1998-10-14 Ethyl Corporation Additives for minimizing intake valve deposits, and their use
EP1277828A2 (en) * 1999-02-09 2003-01-22 Basf Aktiengesellschaft Fuel composition

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7766982B2 (en) 2003-09-25 2010-08-03 Afton Chemical Corporation Fuels compositions and methods for using same
US7491248B2 (en) 2003-09-25 2009-02-17 Afton Chemical Corporation Fuels compositions and methods for using same
EP1518918A1 (en) * 2003-09-25 2005-03-30 Afton Chemical Corporation Fuels compositions and methods for using same
EP1840192A1 (en) 2006-03-30 2007-10-03 Afton Chemical Corporation Treated port fuel injectors
KR100821547B1 (en) * 2006-03-30 2008-04-14 에프톤 케미칼 코포레이션 Treated port fuel injectors
US7422161B2 (en) 2006-03-30 2008-09-09 Afton Chemical Corporation Treated port fuel injectors
US9157041B2 (en) 2007-09-27 2015-10-13 Innospec Limited Fuel compositions
WO2009040584A1 (en) * 2007-09-27 2009-04-02 Innospec Limited Fuel compositions
GB2453249B (en) * 2007-09-27 2010-12-15 Innospec Ltd Fuel compositions
JP2010540711A (en) * 2007-09-27 2010-12-24 インノスペック リミテッド Fuel composition
CN102007203A (en) * 2007-09-27 2011-04-06 因诺斯佩克有限公司 Diesel fuel compositions
GB2453248B (en) * 2007-09-27 2011-11-23 Innospec Ltd Fuel compositions
WO2009040583A1 (en) * 2007-09-27 2009-04-02 Innospec Limited Fuel compositions
US9163190B2 (en) 2007-09-27 2015-10-20 Innospec Limited Fuel compositions
US9243199B2 (en) 2007-09-27 2016-01-26 Innospec Limited Fuel compositions
CN106103667A (en) * 2013-11-18 2016-11-09 雅富顿化学公司 Cleanser compositions for the mixing that inlet valve deposits controls
EP3071677A4 (en) * 2013-11-18 2016-12-28 Afton Chemical Corp Mixed detergent composition for intake valve deposit control
US10457884B2 (en) 2013-11-18 2019-10-29 Afton Chemical Corporation Mixed detergent composition for intake valve deposit control
CN106103667B (en) * 2013-11-18 2019-12-10 雅富顿化学公司 Mixed detergent composition for intake valve deposit control
US10273425B2 (en) 2017-03-13 2019-04-30 Afton Chemical Corporation Polyol carrier fluids and fuel compositions including polyol carrier fluids
US11873461B1 (en) 2022-09-22 2024-01-16 Afton Chemical Corporation Extreme pressure additives with improved copper corrosion
US12024686B2 (en) 2022-09-30 2024-07-02 Afton Chemical Corporation Gasoline additive composition for improved engine performance
US11884890B1 (en) 2023-02-07 2024-01-30 Afton Chemical Corporation Gasoline additive composition for improved engine performance
US11795412B1 (en) 2023-03-03 2023-10-24 Afton Chemical Corporation Lubricating composition for industrial gear fluids

Also Published As

Publication number Publication date
EP1411105A3 (en) 2004-04-28
EP1411105B9 (en) 2009-10-14
DE60103043D1 (en) 2004-06-03
EP1411105B1 (en) 2009-07-08
AU3990201A (en) 2001-09-17
EP1268715A2 (en) 2003-01-02
WO2001066673A3 (en) 2002-03-28
CA2402851A1 (en) 2001-09-13
WO2001066673A2 (en) 2001-09-13
EP1268715B1 (en) 2004-04-28
AU2001239902B2 (en) 2005-06-02
DE60139215D1 (en) 2009-08-20
DE60103043T2 (en) 2004-12-30
US6458172B1 (en) 2002-10-01

Similar Documents

Publication Publication Date Title
EP1268715B1 (en) Fuel additive compositions and fuel compositions containing detergents and fluidizers
AU2001239902A1 (en) Fuel additive compositions and fuel compositions containing detergents and fluidizers
US20030177692A1 (en) Method of operating a direct injection spark-ignited engine with a fuel composition
US6136052A (en) Fuel additives and fuel compositions containing said fuel additive
US8231695B2 (en) Fuel compositions comprising hydrocarbon oil carriers and methods for using the same
KR100749715B1 (en) Fuels compositions and methods for using same
AU2002315108B2 (en) Fuel composition containing detergent combination and methods thereof
JP2744205B2 (en) Fuel composition and additives therefor
AU2002315108A1 (en) Fuel composition containing detergent combination and methods thereof
EP4424801A2 (en) Gasoline additive composition for improved engine performance
RU2695347C2 (en) Methods and applications for control of deposits on valves in engines with spark ignition with direct injection of fuel
US7422161B2 (en) Treated port fuel injectors
EP1812534B1 (en) Additive and fuel compositions containing detergent and fluidizer and method thereof
EP4413100A1 (en) Fuel additives for lowering deposit and particulate emission

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

17P Request for examination filed

Effective date: 20031128

AC Divisional application: reference to earlier application

Ref document number: 1268715

Country of ref document: EP

Kind code of ref document: P

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): DE FR GB NL SE

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): DE FR GB NL SE

AKX Designation fees paid

Designated state(s): DE FR GB NL SE

17Q First examination report despatched

Effective date: 20041222

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AC Divisional application: reference to earlier application

Ref document number: 1268715

Country of ref document: EP

Kind code of ref document: P

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): DE FR GB NL SE

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REF Corresponds to:

Ref document number: 60139215

Country of ref document: DE

Date of ref document: 20090820

Kind code of ref document: P

NLV1 Nl: lapsed or annulled due to failure to fulfill the requirements of art. 29p and 29m of the patents act
PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20090708

PLBI Opposition filed

Free format text: ORIGINAL CODE: 0009260

PLAX Notice of opposition and request to file observation + time limit sent

Free format text: ORIGINAL CODE: EPIDOSNOBS2

26 Opposition filed

Opponent name: NEW MARKET SERVICES CORPORATION

Effective date: 20100408

PLBB Reply of patent proprietor to notice(s) of opposition received

Free format text: ORIGINAL CODE: EPIDOSNOBS3

RDAF Communication despatched that patent is revoked

Free format text: ORIGINAL CODE: EPIDOSNREV1

RDAG Patent revoked

Free format text: ORIGINAL CODE: 0009271

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: PATENT REVOKED

27W Patent revoked

Effective date: 20110106

GBPR Gb: patent revoked under art. 102 of the ep convention designating the uk as contracting state

Effective date: 20110106

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20110309

Year of fee payment: 11

Ref country code: DE

Payment date: 20110225

Year of fee payment: 11

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20110223

Year of fee payment: 11

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20090708